CN101832572B - Method for leading flue gas out of sintering flue gas waste heat utilization system without using induced draft fan - Google Patents
Method for leading flue gas out of sintering flue gas waste heat utilization system without using induced draft fan Download PDFInfo
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- CN101832572B CN101832572B CN2010101279856A CN201010127985A CN101832572B CN 101832572 B CN101832572 B CN 101832572B CN 2010101279856 A CN2010101279856 A CN 2010101279856A CN 201010127985 A CN201010127985 A CN 201010127985A CN 101832572 B CN101832572 B CN 101832572B
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Abstract
The invention discloses a method for leading flue gas out of a sintering flue gas waste heat utilization system without using an induced draft fan and belongs to the technical field of sintering machine flue gas waste heat utilization technology in steel industry. Flue gas on the tail part of a sintering machine enters a waste heat boiler through a tail air box and a flue gas branch pipe to exchange heat with a working medium; after the flue gas exchanges heat with the working medium, low-temperature flue gas enters a non-desulfurated smoke collecting header or a main smoke collecting header of a sintering system through a waste heat boiler flue passage arranged at one end of the waste heat boiler, and is led out and emptied after dust in the low-temperature flue gas is removed by a main exhaust fan in the non-desulfurated smoke collecting header or the main smoke collecting header. Equipment cost as well as running and maintenance costs increased due to the arrangement of an induced draft fan on the tail part of the waste heat boiler in a conventional sintering waste heat utilization system are saved and potential safety hazard to the system caused by running the induced draft fan in a severe environment is eliminated.
Description
Technical field
The invention belongs to steel industry sintering device flue gas UTILIZATION OF VESIDUAL HEAT IN technical field, be particularly related to a kind of sinter fume bootstrap system inducing free fan flue gas outbound course, it is in sinter fume UTILIZATION OF VESIDUAL HEAT IN process, and flue gas does not need the induced draught fan pressurization just can discharge smoothly after residual heat boiler for exchanging heat.
Background technique
Sintering deposit can produce big calorimetric flue gas in sintering process, these hot flue-gas temperatures are between 50 ℃-450 ℃, and sulphur content is between 0mg/L-9000mg/L, and temperature and sulphur content are inhomogeneous along sintering machine length direction distributed pole.Therefore many big-and-middle-sized sintering plants have all optionally carried out purified treatment to sinter fume before discharging: be provided with the female pipe 4 of female pipe 3 of desulfurization collection cigarette and non-desulfurization collection cigarette in sintering machine 1 both sides, the flue gas that sintering machine middle part Sulpher content is high is directed to dedusting after the female pipe 3 of desulfurization collection cigarette compiles, desulfurizer purifies, take discharging away by main exhauster on the female pipe 3 of desulfurization collection cigarette again, and sintering machine 1 head and the low-sulfur content flue gas of afterbody are after the female pipe 4 of non-desulfurization collection cigarette compiles, through dust removal process, extract emptying out by main exhauster on the female pipe 4 of non-desulfurization collection cigarette then again.
Because sintering machine 1 middle part flue gas Sulpher content height, the heat recovery cost is big, and sintering machine head flue-gas temperature is lower and do not have value, and the sinter fume that therefore carries out heat recovery is all taken from the non-desulfurization flue gas of sintering machine afterbody.The exhaust gas volumn that participates in heat recovery will be decided on sintering machine scale and sinter fume temperature, generally be from sintering machine 1 afterbody second-to-last bellows, the flue gas that draws 2-5 afterbody bellows is to exhaust heat boiler 15 heating working medium water, flue gas after the heat exchange is evacuated in female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette by the induced draught fan that is located at exhaust heat boiler back-end ductwork back again, extracted out emptying by main exhauster after dedusting, this is the lead-out mode after the existing sinter fume UTILIZATION OF VESIDUAL HEAT IN.At this, the effect that induced draught fan is set is for flue gas provides enough power, makes it can overcome flue resistance, flow to female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette from the sintering bellows swimmingly.Yet the drawback of this mode is to establish a high-power induced draught fan at boiler tail, has not only increased cost of equipment, and owing to dust loading in the flue gas is big, the induced draught fan work under bad environment is brought hidden danger to system safety operation simultaneously.
Summary of the invention
The cost of equipment that exists at lead-out mode after the existing sinter fume UTILIZATION OF VESIDUAL HEAT IN increases, there is the deficiency of hidden danger in system's operation, the present invention aims to provide a kind of sinter fume bootstrap system inducing free fan flue gas outbound course, this method only relies on the main exhauster on female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette just can be with the whole carrying-offs of the flue gas after the UTILIZATION OF VESIDUAL HEAT IN, and the system that do not influence normally moves.
For achieving the above object, technological scheme that the present invention adopts is: a kind of sinter fume bootstrap system inducing free fan flue gas outbound course, be provided with female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette in sintering machine one side, be communicated with a plurality of afterbody bellows with the afterbody of sintering machine, afterbody bellows one end is connected with afterbody bellows arm, this afterbody bellows arm is communicated with female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette, on afterbody bellows arm, be provided with the flue gas arm that is communicated with it near the afterbody bellows, this flue gas arm is communicated with exhaust heat boiler via advancing the female pipe of exhaust-heat boiler flue gas, its structural feature is that the other end of described exhaust heat boiler is communicated with by female pipe of exhaust heat boiler back-end ductwork and non-desulfurization collection cigarette or the female pipe of main collection cigarette; Be provided with afterbody bellows manifold valve on the described afterbody bellows arm and between flue gas arm and female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette; Described flue gas arm is provided with the flue gas manifold valve; Be provided with between the flue gas manifold valve on described afterbody bellows manifold valve and the flue gas arm and open and close interlocking; Concrete flue gas outbound course is: the aperture of regulating afterbody bellows manifold valve and flue gas manifold valve, make the flue resistance in the exhaust heat boiler not be higher than 800Pa, rely on the main exhauster in female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette the low-temperature flue gas after the dedusting can be drawn emptying.
The so-called interlocking that opens and closes is afterbody bellows manifold valve aperture when turning down, and flue gas manifold valve aperture is transferred big automatically; When afterbody bellows manifold valve is closed fully, the automatic complete opening of flue gas manifold valve; And during afterbody bellows manifold valve complete opening, the flue gas manifold valve is closed automatically fully.
When sintering machine ordinary production or underrun, afterbody bellows manifold valve is finished surplus closing, the automatic complete opening of flue gas manifold valve, sinter fume is collected to the into female pipe of exhaust-heat boiler flue gas from each flue gas arm, advance the sintering waste heat boiler again, heat exchange in stove is extracted emptying out by main exhauster after boiler back end ductwork and the electronic baffle plate of exhaust heat boiler tail flue gas are pumped down to female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette then again after the deduster dedusting.
When the sintering machine high load running, regulate the aperture of afterbody bellows manifold valve, the flue gas manifold valve suitably turns down automatically, this moment, the fraction sinter fume was flowed directly to female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette from afterbody bellows arm, most of sinter fume is collected to the into female pipe of exhaust-heat boiler flue gas through each flue gas arm, advances sintering waste heat boiler and working medium heat exchange again.。
Described afterbody bellows manifold valve is for controlling the mortor operated valve of the flue gas flow that enters female pipe of non-desulfurization collection cigarette or main collection cigarette mother pipe automatically; The flue gas manifold valve enters the interior flue gas flow of exhaust heat boiler and the mortor operated valve of flue gas resistance for controlling automatically.
Be provided with the electronic baffle plate of exhaust heat boiler tail flue gas in the described exhaust heat boiler back-end ductwork.
Sinter fume flow to exhaust heat boiler from sintering machine afterbody bellows, flow to female pipe of non-desulfurization collection cigarette or the emptying of the female pipe of main collection cigarette again, the power of whole flow process is provided by main exhauster intakeport pressure by air pressure difference in blast in the sintering machine afterbody bellows and female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette; In equipment and pipeline that sinter fume is flowed through, maximum flow resistance is from the flue resistance in the exhaust heat boiler, this part resistance accounts for more than 2/3 of whole flue resistances, therefore, if require to guarantee flue gas smooth and easy circulation under the situation of not establishing induced draught fan, the flue resistance that must control in the exhaust heat boiler is not higher than 800Pa, thereby realize that the exhaust heat boiler back-end ductwork do not establish induced draught fan, only by the main exhauster suction force in female pipe of the existing non-desulfurization collection cigarette of sintering system or the female pipe of main collection cigarette and make sinter fume at sintering machine afterbody bellows, the flue gas arm, exhaust heat boiler, female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette, smooth and easy circulation between the deduster.
The present invention realizes that the key of its technique effect is the flue resistance of rationally controlling in the exhaust heat boiler, make exhaust heat boiler inner flue resistance and system's smoke pipe resistance sum suction force less than main exhauster, flue gas could flow to female pipe of non-desulfurization collection cigarette or the female pipe of main collection cigarette from sintering machine wind box swimmingly like this, is taken away by main exhauster.
Below the present invention made further specify.
Referring to shown in Figure 1, according to sintering machine 1 tail flue gas amount and flue-gas temperature situation, from sintering machine 1 afterbody second-to-last afterbody bellows, the flue gas that draws 2～5 afterbody bellows 9 advances exhaust heat boiler 15; Installing afterbody bellows manifold valve 11 on the afterbody bellows arm 10 of several afterbody bellows 9 of utilizing that has surplus heat, before the afterbody bellows manifold valve 11 of afterbody bellows arm 10, be installed up to the flue gas arm 12 of exhaust heat boiler 15, and on flue gas arm 12, install flue gas manifold valve 13, between afterbody bellows manifold valve 11 and flue gas manifold valve 13, be provided with and open and close interlocking; The so-called interlocking that opens and closes is afterbody bellows manifold valve 11 apertures when turning down, and flue gas manifold valve 13 apertures are transferred big automatically; When afterbody bellows manifold valve 11 is closed fully, flue gas manifold valve 13 automatic complete openings; And during afterbody bellows manifold valve 11 complete openings, flue gas manifold valve 13 is closed automatically fully.
When sintering machine 1 ordinary production or underrun, afterbody bellows manifold valve 11 is closed fully, flue gas manifold valve 13 automatic complete openings, sinter fume is collected to female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette from each flue gas arm 12, enter heat exchange in the sintering waste heat boiler 15 again, heat exchange in stove is extracted emptying out by main exhauster after the electronic baffle plate 17 of boiler back end ductwork 16 and exhaust heat boiler tail flue gas is pumped down to female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette then again after the deduster dedusting.
When sintering machine 1 high load running, regulate the aperture of afterbody bellows manifold valve 11, flue gas manifold valve 13 suitably turns down automatically, this moment, a part of sinter fume was flowed directly to female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette from afterbody bellows arm 10, another part sinter fume is collected to the into female pipe 14 of exhaust-heat boiler flue gas through each flue gas arm 12, enter heat exchange in the sintering waste heat boiler 15 again, heat exchange in stove is after the electronic baffle plate 17 of boiler back end ductwork 16 and exhaust heat boiler tail flue gas, be pumped down to female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette then, after the deduster dedusting, extract emptying out by main exhauster again.
When sintering machine 1 start and stop or bootstrap system maintenance, flue gas manifold valve 13 is closed fully, afterbody bellows manifold valve 11 automatic complete openings, and flue gas flow to the female pipe 4 of non-desulfurization collection cigarette by afterbody bellows arm 10, does not advance exhaust heat boiler 15.
Compared with prior art, the invention has the beneficial effects as follows: the present invention has cancelled the way of existing sinter fume extraction system at an induced draught fan of exhaust heat boiler afterbody installing, the main exhauster that only relies on female pipe of non-desulfurization collection cigarette or master to collect on the female pipe of cigarette just can be with the whole carrying-offs of the flue gas after the UTILIZATION OF VESIDUAL HEAT IN, and the system that do not influence normally moves, saved existing sintering waste heat and utilized system to need cost of equipment and the operating maintenance expense that increases at exhaust heat boiler afterbody installing induced draught fan, eliminated induced draught fan and under rugged environment, moved the potential safety hazard of bringing to system; Employed apparatus structure is simple, and is easy to operate, and energy conservation and consumption reduction effects is obvious.
Description of drawings
Fig. 1 is the manufacturing process control schematic representation of an embodiment of the present invention.
In the drawings:
The 1-sintering machine, the 2-sintering deposit,
The female pipe of 3-desulfurization collection cigarette, the female pipe of the non-desulfurization collection of 4-cigarette,
5-head bellows, 6-head bellows arm,
7-middle part bellows, 8-middle part bellows arm,
9-afterbody bellows, 10-afterbody bellows arm,
11-afterbody bellows manifold valve, 12-flue gas arm,
13-flue gas manifold valve, 14-advances the female pipe of exhaust-heat boiler flue gas,
The 15-exhaust heat boiler, 16-exhaust heat boiler back-end ductwork,
The electronic baffle plate of 17-exhaust heat boiler tail flue gas.
Embodiment
A kind of sinter fume bootstrap system inducing free fan flue gas outbound course, as shown in Figure 1, be provided with the female pipe 4 of non-desulfurization collection cigarette in sintering machine 1 one sides, be communicated with 4 afterbody bellows 9 with the afterbody of sintering machine 1, afterbody bellows 9 one ends are connected with afterbody bellows arm 10, this afterbody bellows arm 10 is communicated with the female pipe 4 of non-desulfurization collection cigarette, on afterbody bellows arm 10, be provided with the flue gas arm 12 that is communicated with it near afterbody bellows 9, this flue gas arm 12 is communicated with exhaust heat boiler 15 via advancing the female pipe of exhaust-heat boiler flue gas 14, and the other end of described exhaust heat boiler 15 is managed 4 by exhaust heat boiler back-end ductwork 16 and non-desulfurization collection cigarette mother and is communicated with; Be provided with afterbody bellows manifold valve 11 on the described afterbody bellows arm 10 and between flue gas arm 12 and the female pipe 4 of non-desulfurization collection cigarette; Described flue gas arm 12 is provided with flue gas manifold valve 13; Be provided with between described afterbody bellows manifold valve 11 and the flue gas manifold valve 13 and open and close interlocking.
Described exhaust heat boiler back-end ductwork 16 is provided with the electronic baffle plate 17 of exhaust heat boiler tail flue gas.
Described afterbody bellows manifold valve 11 enters the mortor operated valve of the exhaust gas volumn size of female pipe 4 of non-desulfurization collection cigarette or the female pipe of main collection cigarette for control automatically, and described flue gas manifold valve 13 enters the exhaust gas volumn size in the exhaust heat boiler 15 and the mortor operated valve of flue resistance for control automatically.
The so-called interlocking that opens and closes is afterbody bellows manifold valve 11 apertures when turning down, and flue gas manifold valve 13 apertures are transferred big automatically; When afterbody bellows manifold valve 11 is closed fully, flue gas manifold valve 13 automatic complete openings; And during afterbody bellows manifold valve 11 complete openings, flue gas manifold valve 13 is closed automatically fully.
Concrete flue gas outbound course is:
When sintering machine 1 ordinary production or underrun, afterbody bellows manifold valve 11 is closed fully, flue gas manifold valve 13 automatic complete openings, sinter fume is collected to the female pipe 4 of non-desulfurization collection cigarette from each flue gas arm 12, enter heat exchange in the sintering waste heat boiler 15 again, heat exchange in stove is extracted emptying out by main exhauster after the electronic baffle plate 17 of boiler back end ductwork 16 and exhaust heat boiler tail flue gas is pumped down to the female pipe 4 of non-desulfurization collection cigarette then again after the deduster dedusting.
When sintering machine 1 high load running, automatically regulate the aperture of afterbody bellows manifold valve 11, flue gas manifold valve 13 suitably turns down automatically, this moment, a part of sinter fume was flowed directly to the female pipe 4 of non-desulfurization collection cigarette from afterbody bellows arm 10, another part sinter fume is collected to the into female pipe 14 of exhaust-heat boiler flue gas through each flue gas arm 12, enter heat exchange in the sintering waste heat boiler 15 again, heat exchange in stove is after the electronic baffle plate 17 of boiler back end ductwork 16 and exhaust heat boiler tail flue gas, be pumped down to the female pipe 4 of non-desulfurization collection cigarette then, after the deduster dedusting, extract emptying out by main exhauster again.
When sintering machine 1 start and stop or bootstrap system maintenance, flue gas manifold valve 13 is closed fully, afterbody bellows manifold valve 11 automatic complete openings, and flue gas flow to the female pipe 4 of non-desulfurization collection cigarette by afterbody bellows arm 10, does not advance exhaust heat boiler 15.
Different with existing sinter fume bootstrap system, the present invention does not establish induced draught fan on exhaust heat boiler back-end ductwork 16, sinter fume flow to exhaust heat boiler 15 from sintering machine 1 afterbody bellows 9 through flue gas arm 12, flow to emptying in the female pipe 4 of non-desulfurization collection cigarette again, the power of whole flow process is provided by the main exhauster intakeport pressure by air pressure difference in blast in the sintering machine 1 afterbody bellows 9 and the female pipe 4 of non-desulfurization collection cigarette.In equipment and pipeline that sinter fume is flowed through, maximum flow resistance is from exhaust heat boiler 15 inner flue resistances, this part resistance accounts for more than 2/3 of whole flue resistances, and therefore, the flue resistance in the control exhaust heat boiler is the key that guarantees flue gas smooth and easy circulation under the situation of not establishing induced draught fan.When flue gas resistance was no more than 800Pa in the exhaust heat boiler, flue gas can smooth and easy circulation, and through appropriate design, the flue gas resistance under prior art in the control boiler 15 is not higher than 800Pa can be realized fully.
Method and apparatus of the present invention both had been applicable to that the fume afterheat of the sintering machine that is provided with the female pipe of the female Guan Yufei desulfurization of desulfurization collection cigarette collection cigarette utilized system; also be applicable to and only establish a female pipe of main collection cigarette; and the hot fume afterheat of the sintering machine of the sinter fume separate collection not being handled utilizes system; therefore the present invention is not establishing the female pipe of two collection of desulfurization and non-desulfurization cigarette, and has only the application on the sintering machine of a main collection cigarette mother pipe also should be protected.
Claims (3)
1. sinter fume bootstrap system inducing free fan flue gas outbound course, be provided with female pipe of non-desulfurization collection cigarette (4) or the female pipe of main collection cigarette in sintering machine (1) one side, be communicated with a plurality of afterbody bellows (9) with the afterbody of sintering machine (1), afterbody bellows (9) one ends are connected with afterbody bellows arm (10), this afterbody bellows arm (10) is communicated with female pipe of non-desulfurization collection cigarette (4) or the female pipe of main collection cigarette, go up close afterbody bellows (9) at afterbody bellows arm (10) and be provided with the flue gas arm (12) that is communicated with it, this flue gas arm (12) is communicated with exhaust heat boiler (15) via advancing the female pipe of exhaust-heat boiler flue gas (14), it is characterized in that the other end of described exhaust heat boiler (15) is communicated with female pipe of non-desulfurization collection cigarette (4) or the female pipe of main collection cigarette by exhaust heat boiler back-end ductwork (16); Described afterbody bellows arm (10) is gone up and is positioned between flue gas arm (12) and female pipe of non-desulfurization collection cigarette (4) or the female pipe of main collection cigarette and is provided with afterbody bellows manifold valve (11); Described flue gas arm (12) is provided with flue gas manifold valve (13); Be provided with between the flue gas manifold valve (13) on described afterbody bellows manifold valve (11) and the flue gas arm (12) and open and close interlocking; Concrete flue gas outbound course is: the aperture of regulating afterbody bellows manifold valve (11) and flue gas manifold valve (13), make the flue gas resistance in the exhaust heat boiler (15) not be higher than 800Pa, rely on the main exhauster in female pipe of non-desulfurization collection cigarette (4) or the female pipe of main collection cigarette the low-temperature flue gas after the dedusting can be drawn emptying.
2. according to the described sinter fume bootstrap system of claim 1 inducing free fan flue gas outbound course, it is characterized in that described afterbody bellows manifold valve (11) is for controlling the mortor operated valve of the flue gas flow that enters female pipe of non-desulfurization collection cigarette (4) or main collection cigarette mother pipe automatically; Flue gas manifold valve (13) enters the interior flue gas flow of exhaust heat boiler (15) and the mortor operated valve of flue gas resistance for controlling automatically.
3. according to the described sinter fume bootstrap system of claim 1 inducing free fan flue gas outbound course, it is characterized in that, be provided with the electronic baffle plate of exhaust heat boiler tail flue gas (17) in the described exhaust heat boiler back-end ductwork (16).
Priority Applications (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN2010101279856A CN101832572B (en) | 2010-03-19 | 2010-03-19 | Method for leading flue gas out of sintering flue gas waste heat utilization system without using induced draft fan |
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| Application Number | Priority Date | Filing Date | Title |
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| CN2010101279856A CN101832572B (en) | 2010-03-19 | 2010-03-19 | Method for leading flue gas out of sintering flue gas waste heat utilization system without using induced draft fan |
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| CN101832572A CN101832572A (en) | 2010-09-15 |
| CN101832572B true CN101832572B (en) | 2011-10-12 |
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| CN2010101279856A Expired - Fee Related CN101832572B (en) | 2010-03-19 | 2010-03-19 | Method for leading flue gas out of sintering flue gas waste heat utilization system without using induced draft fan |
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| CN103615908B (en) * | 2013-12-11 | 2015-03-11 | 北京志能祥赢节能环保科技有限公司 | Combined waste heat recycling system for stepping-type flat-burning sintering machine |
| CN108613211A (en) * | 2018-06-08 | 2018-10-02 | 江苏双良新能源装备有限公司 | A kind of bypass type flue gas waste heat recovery system and its take cigarette control method |
| CN111366003A (en) * | 2020-03-25 | 2020-07-03 | 攀钢集团攀枝花钢钒有限公司 | Sintering flue gas waste heat utilization structure in desulfurization and denitrification system |
Family Cites Families (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| JPS63241124A (en) * | 1987-03-27 | 1988-10-06 | Sumitomo Metal Ind Ltd | Method for controlling temperature of circulating gas for sintering |
| JP2599522B2 (en) * | 1991-10-25 | 1997-04-09 | 新日本製鐵株式会社 | Sintering operation method |
| JP2000105084A (en) * | 1998-07-31 | 2000-04-11 | Nkk Corp | Exhaust gas treating method and apparatus for sintering machine |
| CN101118125A (en) * | 2007-09-14 | 2008-02-06 | 昆明阳光基业股份有限公司 | Smelting sintered ring-cold heat-recovering generating plant and method thereof |
| CN201218660Y (en) * | 2008-04-24 | 2009-04-08 | 西安思安新能源有限公司 | Power generation apparatus by waste heat of sintering production |
| CN201289314Y (en) * | 2008-10-14 | 2009-08-12 | 中国船舶重工集团公司第七○三研究所 | System for recirculating outlet flue gas of sintering device exhaust-heat boiler |
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Address after: 410329 Liuyang City, Hunan Province, the National Bio pharmaceutical industry base (next to the national highway 319) Patentee after: YONKER ENVIRONMENTAL PROTECTION Co.,Ltd. Address before: 410005 Changsha Furong Road, Hunan, No. 2, No. 80, the international Fortune Center, floor, floor, building 15 Patentee before: Hunan Yonker Environmental Protection Co.,Ltd. |
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Effective date of registration: 20170123 Address after: 410330, Liuyang economic and Technological Development Zone, Hunan, blue road, No. 6 Patentee after: Yongqing Hunan investment Refco Group Ltd. Address before: 410329 Liuyang City, Hunan Province, the National Bio pharmaceutical industry base (next to the national highway 319) Patentee before: YONKER ENVIRONMENTAL PROTECTION Co.,Ltd. |
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Granted publication date: 20111012 Termination date: 20190319 |